Hulst A C, Tramper J, Van't Riet K, Westerbeek J M
Agricultural University, Department of Food Science, Food and Bioengineering Group, De Dreyen 12, 6703 BC Wageningen, The Netherlands.
Biotechnol Bioeng. 1985 Jun;27(6):870-6. doi: 10.1002/bit.260270617.
A new technique is presented for the production of immobilized biocatalysts in large quantities. It consists of breaking up a jet of the biocatalyst/presupport mixture in uniform droplets by means of a resonance technique. Entrapment of yeast and plant cells in calcium alginate has been used as the model. The production capacity of the nozzles used (0.5, 0.8, and 1.1 mm exit diameters) is two orders of magnitude larger than the production capacity of the conventional techniques (maximum capacity with a 1.1-mm nozzle diameter is 24 L/h). Depending on frequency, nozzle diameter, and volumetric flow rate, the bead size varies between 1 and 2 mm, with standard deviations of 3-5% for yeast immobilization and 10-15% for plant cells. The deactivation of both yeast and plant cells is small and comparable to that found in the corresponding conventional procedures.
本文介绍了一种大量生产固定化生物催化剂的新技术。该技术通过共振技术将生物催化剂/预载体混合物的射流破碎成均匀的液滴。以酵母和植物细胞包埋于海藻酸钙中作为模型。所用喷嘴(出口直径0.5、0.8和1.1毫米)的生产能力比传统技术的生产能力大两个数量级(1.1毫米喷嘴直径的最大生产能力为24升/小时)。根据频率、喷嘴直径和体积流速,珠粒尺寸在1至2毫米之间变化,酵母固定化的标准偏差为3 - 5%,植物细胞的标准偏差为10 - 15%。酵母和植物细胞的失活都很小,与相应传统方法中的失活情况相当。